Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
230 words
A process for hydrotreating hydrocarbon feeds comprising contacting a hydrocarbon feed with hydrogen under hydrotreating conditions in the presence of a catalyst composition comprising a hydrogenating component and a support comprising at least one porous refractory inorganic oxide, said catalyst having a BET surface area of 150 to about 190 m 2 /g, bulk density of at least about 0.2 g/cc, total pore volume equal to the sum of micropore volume determined by nitrogen desorption in micropores having radii up to 600 Å and macropore volume determined by mercury penetration in macropores having radii of 600 to 25,000 Å of at least 0.9 cc/g, with at least 0.1 cc/g of macropore volume, such surface area, pore size distribution and total pore volume being effective to provide an average pore diameter of at least 230 Å calculated as 4 V/A, wherein at least 0.7 cc/g of the micropore volume is concentrated in pores having radii of 50 to 600 Å, wherein the micropore volume in pores having radii of 50 to 600 Å is distributed such that about 15 to about 60% thereof is provided by pores having radii of 50 to 100 Å and about 40 to about 85% thereof is provided by pores having radii of 100 to 600 Å, and wherein the micropore volume in pores having radii less than 50 Å is less than about 0.15 cc/g.
Claim 2
Dependent Claim
230 words
A process for hydrotreating hydrocarbon feeds comprising contacting a hydrocarbon feed with hydrogen under hydrotreating conditions in the presence of a catalyst composition comprising a hydrogenating component and a support comprising at least one porous refractory inorganic oxide, said catalyst having a BET surface area of 150 to about 190 m 2 /g, bulk density of at least about 0.2 g/cc, total pore volume equal to the sum of micropore volume determined by nitrogen desorption in micropores having radii up to 600 Å and macropore volume determined by mercury penetration in macropores having radii of 600 to 25,000 Å of at least 0.9 cc/g, with at least 0.1 cc/g of macropore volume, such surface area, pore size distribution and total pore volume being effective to provide an average pore diameter of at least 230 Å calculated as 4 V/A, wherein at least 0.7 cc/g of the micropore volume is concentrated in pores having radii of 50 to 600 Å, wherein the micropore volume in pores having radii of 50 to 600 Å is distributed such that about 15 to about 60% thereof is provided by pores having radii of 50 to 100 Å and about 40 to about 85% thereof is provided by pores having radii of 100 to 600 Å, and wherein the micropore volume in pores having radii less than 50 Å is less than about 0.15 cc/g.
Claim 3
Dependent Claim
72 words
The process of claim 1 wherein the hydrocarbon feed comprises a distillate and hydrotreating conditions comprise a pressure of about 300 to about 750 psig (about 21 to about 53 kg/cm 2 ), temperature of about 600° to about 725° F. (about 315° to about 385° C.), hydrogen rate of about 400 to about 1000 SCFB and space velocity of about 2 to about 5 lb hydrocarbon per hour per lb catalyst.
Claim 4
Dependent Claim
73 words
The process of claim 1 wherein the hydrocarbon feed comprises a gas oil and hydrotreating conditions comprise a pressure of about 500 to about 1000 psig (about 35 to about 70 kg/cm 2 ), temperature of about 600° to about 750° F. (about 315° to about 399° C.), hydrogen rate of about 800 to about 1600 SCFB and space velocity of about 1 to about 4 lb hydrocarbon per hour per lb catalyst.
Claim 5
Dependent Claim
73 words
The process of claim 1 wherein the hydrocarbon feed comprises an atmsopheric or vacuum resid and hydrotreating conditions comprise a pressure of about 500 to about 10,000 psig (about 35 to about 703 kg/cm 2 ), temperature of about 600° to about 950° F. (about 315° to about 510° C.), hydrogen rate of about 1000 to 10,000 SCFB and space velocity of about 0.2 to about 3 lb hydrocarbon per hour lb. catalyst.
Claim 6
Dependent Claim
30 words
The process of claim 1 wherein the hydrogenating component comprises at least one metal selected from the group consisting of the Group VIB metals, the Group VIII metals and vanadium.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein the hydrogenating component comprises molybdenum.
Claim 8
Dependent Claim
25 words
The process of any of claims 1-6 wherein the hydrocarbon feed and hydrogen are contacted in the presence of a fixed bed of said catalyst.
Claim 9
Dependent Claim
25 words
The process of any of claims 1-6 wherein the hydrocarbon feed and hydrogen are contacted in the presence of an expanded bed of said catalyst.